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Method for recovering cobalt from zinc-cobalt-nickel slag purified by zinc hydrometallurgy

A technology of hydrometallurgy and zinc purification, applied in the direction of improving process efficiency, etc., can solve problems such as difficult recovery of cobalt, achieve the effects of improving cobalt recovery rate, reducing unit consumption, and easy process control

Pending Publication Date: 2022-03-15
云南云铜锌业股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In view of the above-mentioned deficiencies in the prior art, the purpose of the present invention is to provide a method for recovering cobalt from zinc-cobalt-nickel slag purified by zinc hydrometallurgy, aiming at solving the difficulty of cobalt recovery in existing zinc-cobalt-nickel slag purified by zinc hydrometallurgy The problem

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0059] Purified zinc-cobalt-nickel slag is provided, the pre-leaching solution with an acid concentration of 250g / l is configured and heated to 85°C, and then the purified zinc-cobalt-nickel slag is added according to a liquid-solid mass ratio of 1:3 to carry out an acid leaching reaction. The reaction time of one acid leaching is 2 hours, and the acidity of the terminal system of the one acid leaching reaction is 0.2 g / l. After the completion of the one acid leaching reaction, filter is carried out to obtain the liquid after the first acid leaching and the residue of the first acid leaching.

[0060] Heat the pre-leaching solution with an acid concentration of 250g / l to 85°C, add the primary acid leaching residue according to the liquid-solid mass ratio of 5:1, and perform a secondary acid leaching reaction. The reaction of the secondary acid leaching reaction The time is 3 hours, the acidity of the system at the end point of the secondary acid leaching reaction is 17 g / l, and...

Embodiment 2

[0063] Purified zinc-cobalt-nickel slag is provided, the pre-leaching solution with an acid concentration of 200g / l is configured and heated to 85° C., and then the purified zinc-cobalt-nickel slag is added according to a liquid-solid mass ratio of 1:5 to carry out an acid leaching reaction. The reaction time of one acid leaching is 3 hours, and the acidity of the terminal system of the one acid leaching reaction is 1 g / l. After the completion of the one acid leaching reaction, it is filtered to obtain the liquid after the first acid leaching and the residue of the first acid leaching.

[0064] The pre-leaching solution with an acid concentration of 200g / l was heated to 85°C, and continued to add the primary acid leaching residue according to the liquid-solid ratio of 5:1 to carry out the secondary acid leaching reaction, and the secondary acid leaching reaction The reaction time is 2 hours, the acidity of the secondary acid leaching reaction terminal system is 5g / l, and the li...

Embodiment 3

[0067] Purified zinc-cobalt-nickel slag is provided, the pre-leaching solution with an acid concentration of 300g / l is configured and heated to 85°C, and then the purified zinc-cobalt-nickel slag is added according to a liquid-solid mass ratio of 1:2 to carry out an acid leaching reaction. The reaction time of one acid leaching is 3 hours, the pH of the system at the end of the first acid leaching reaction is 3.5, and after the completion of the first acid leaching reaction, filter to obtain the solution after the first acid leaching with a Co content of 6.18g / l.

[0068] Heat the solution after primary acid leaching with a Co content of 6.18g / l to 85°C, add ammonium salt which is 3 times the theoretically calculated amount, and carry out an oxidation reaction. The reaction time of the oxidation reaction is 5h, and after filtration, a Co 23% cobalt concentrate.

[0069] In summary, the present invention provides a method for recovering cobalt from zinc-cobalt-nickel slag purif...

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Abstract

The invention discloses a method for recovering cobalt from purified zinc-cobalt-nickel slag in zinc hydrometallurgy, which comprises the following steps: providing purified zinc-cobalt-nickel slag; preparing a leaching pre-solution with a certain acid concentration, heating the leaching pre-solution, then adding the purified zinc-cobalt-nickel slag to carry out a primary acid leaching reaction, and filtering to obtain a primary acid-leached post-solution and primary acid-leached slag; and after the primary acid leaching post-liquid is heated, ammonium salt or sodium salt is added for an oxidation reaction, and cobalt concentrate and cobalt-removed post-liquid are obtained after filtering. And the primary acid leaching residue is continuously subjected to secondary acid leaching reaction. Cyclic enrichment of cobalt in the system during purification slag treatment through a conventional method is avoided, unit consumption of zinc powder is reduced, the cobalt recovery rate is increased, high-grade cobalt concentrate is obtained, and the cobalt content of the cobalt concentrate is 23%-26%. The method provided by the invention is simple to operate, the process is easy to control, the cobalt content of the obtained cobalt concentrate is relatively high, cobalt in the purified slag is recycled to the maximum extent, the value of valuable metals is improved, and quality improvement and efficiency improvement are realized.

Description

technical field [0001] The invention relates to the field of non-ferrous metal smelting, in particular to a method for recovering cobalt from zinc-cobalt-nickel slag purified by hydrometallurgy. Background technique [0002] In the process of zinc hydrometallurgy, the supernatant produced by neutral leaching of zinc calcine contains copper, cadmium, cobalt, nickel and other impurity elements. In order to meet the quality requirements of zinc electrowinning solution, the impurities are purified to obtain qualified The zinc sulfate solution is sent to the zinc electrowinning system. The antimony salt purification method is currently the most widely used purification method in the world. During the purification and cobalt removal process, the cobalt in the solution is removed by adding an antimony activator to obtain a purification slag containing Zn-Co-Ni. The purification slag contains high zinc content. In order to recover the zinc, the Zn-Co-Ni purification slag is pickled...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B23/00
CPCC22B7/007C22B23/043Y02P10/20
Inventor 姜艳邱伟佳周中华吴钧徐宏凯刘建平李国峰张少博王赛刘迅刘自虎陈文昌
Owner 云南云铜锌业股份有限公司
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